JP2004174434A - Sludge recovering filter cloth and dewatering filter using the same - Google Patents

Sludge recovering filter cloth and dewatering filter using the same Download PDF

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Publication number
JP2004174434A
JP2004174434A JP2002346199A JP2002346199A JP2004174434A JP 2004174434 A JP2004174434 A JP 2004174434A JP 2002346199 A JP2002346199 A JP 2002346199A JP 2002346199 A JP2002346199 A JP 2002346199A JP 2004174434 A JP2004174434 A JP 2004174434A
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Japan
Prior art keywords
sludge
filter cloth
filter
major axis
filtration
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JP2002346199A
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JP3796737B2 (en
Inventor
Hidemasa Kamitsuma
英征 上妻
Sakae Tanikame
栄 谷亀
Noriyuki Saito
典之 斎藤
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Kizai KK
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Kizai KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a sludge recovering filter cloth for effectively and speedily treating and recovering useful and valuable sludge, and at the same time, economically and speedily recovering a useful metal from a plating liquid containing useful plating metal sludge, and a dewatering filter using the same. <P>SOLUTION: The filter cloth for performing solid-liquid separation in which nicks having a width smaller than the major axis of sludge particles to be recovered and a length larger than the major axis thereof are provided only at the bottom face and at the lower part of the side face of the filter cloth in such a distribution state as to become the sufficient filtration speed, is used for performing the solid-liquid separation by circulating and treating the treatment water containing the sludge for sludge filtration recovery, in the dewatering filter. The dewatering filter is characterized using the filter cloth. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、産業活動等により頻繁に発生する各種懸濁液、特にメッキ処理液から瀘過分離のために適用される、スラッジ回収瀘布、及びそのスラッジ回収瀘布を用いた脱水瀘過装置に関する。即ち、本発明は、ある程度使用されたメッキ浴液(メッキ剥離液、メッキ剥離溶液を含む)をロ過処理して、その中に含有する有価スラッジを回収するスラッジ回収瀘布、及びそのスラッジ回収瀘布を用いた脱水瀘過装置に関する。
【0002】
【従来の技術】
従来の瀘過の技術としては重力瀘過、加圧瀘過、吸引瀘過などの種々のものがあるが、近年では、各種の膜、フィルター、瀘布を利用する技術が多く研究されているが、メッキ膜が剥離したもので懸濁した瀘液を清浄化すると同時に価値のある金属スラッジを回収するために用いると、目詰まりしてしまい、良好な瀘布、ロ過装置が見つからなかった。
【0003】
現在、スラッジ回収瀘布は、従来の重力ロ過装置では、瀘材と瀘過槽が一体となっているために、瀘布に目詰まりを起こしやすく、その問題を解決するためには面倒であり、多くの作業の必要があったが、液差圧により瀘過を行う浸漬式重力瀘過装置が、提案されている(特開2000−189718号参照)。然し乍ら、従来の瀘布では、目詰まりを起こし易いスラッジ、沈殿物でも、効率的に且つ高い速度で固液を分離することができなかった。
【0004】
【発明が解決しようとする課題】
本発明は、スラッジ回収瀘布とそれによる脱水瀘過装置を提供しようとするものである。即ち、本発明は、有用で価値あるスラッジを効率的に且つ迅速に処理し回収するためのものである。同時に、本発明は、有用のメッキ金属スラッジを含有するメッキ液から有用な金属を経済的に且つ迅速に回収するためのものである。
【0005】
【課題を解決するための手段】
本発明者は、上記のような課題を解決すべく鋭意研究を重ねてきた。その結果、次のような手段により、それを解決したものである。
(1)瀘布の底面及び側面の低部のみに、回収すべきスラッジの長径より小さい幅で、該長径より大きい長さの切り目を、十分な瀘過速度になる分布状態で設けた、スラッジ瀘別回収のために、該スラッジを含有する処理液を循環して処理して、固液分離するために、脱水瀘過装置において、使用することを特徴とする固液分離のための瀘布。
【0006】
(2)切り目の幅は、回収すべきスラッジの最も大きい長径より小さく、そして、切り目の長さは、該最大長径より大きいした固液分離のための瀘布。
(3)瀘布の底面及び側面の低部のみに、回収すべきスラッジの長径より小さい幅で、該長径より大きい長さの切り目を、十分な瀘過速度になる分布状態で設けた、瀘布を備えて、該スラッジを含有する処理液を循環して処理して、固液分離するために使用することを特徴とする固液分離のための脱水瀘過装置。
【0007】
以下、本発明のスラッジ回収瀘布とそれを用いた脱水瀘過装置の例を説明するが、本発明は、それにより限定を受けるものではない。
本発明は、瀘布の底面及び側面の低部のみに、回収すべきスラッジの長径より小さい幅で、該長径より大きい長さの切り目(A)を、十分な瀘過速度になる分布状態で設けることにより、スラッジ瀘別回収を効率的に為すようにしたものである。すなわち、切り目(A)は、瀘別されるべきスラッジの形状が長細いものであり、その長い径のところで、瀘布の目に目詰まりして、多量のスラッジがランダムに並んだ状態で、瀘布上に堆積すると、その堆積したスラッジ自体により目詰まりして、円滑に液が処理できなくなる。そこで、本発明では、瀘布に以上の規定の孔を多数設けて、そこを通過するスラッジがあっても、目詰まりがなく、何回かの循環により、回収すべきスラッジのほとんどが、堆積スラッジにひっかかり、堆積して、回収できるようにしたものである。即ち、本発明は、処理液を一部循環させながら、有用なスラッジを回収し、脱水する瀘布とそれを用いた脱水瀘過装置である。
【0008】
本発明によると、通常の瀘布を用いていながら、目詰まりがなく、瀘過速度を確保でき、瀘過循環速度を高くして、ほとんどのスラッジを効率的に且つ迅速に回収することができる。即ち、それは、切り目の幅は、回収すべきスラッジの最も大きい長径より小さく、そして、切り目の長さは、該最大長径より大きいことにより、瀘布の目を詰まらせることなく、処理液を迅速に循環処理することにより、迅速に固液を分離することができる。
【0009】
【発明の実施の形態】
本発明のスラッジ回収の脱水瀘過装置の概略を、図1の断面図で示す。
処理液Bは、入口(1)から、瀘過筒(8)の上段空間に入り、通過穴(3−1)の付いた瀘布押さえ板(3)を通り、瀘布(4)内に入る。そして、瀘布(4)を通過した液は、ネット(網)(7)を通り、瀘過バスケット(6)の下部の穴から、瀘過筒(8)の下段空間に入り、液出口(10)から、外部に出る。ネット(網)(7)は、3層構造(図4参照)であり、瀘布(4)の側面部を通過した液は、その3層構造の網(7)の間を通って、瀘過バスケット(6)の下部穴(6−1)に到達し、そこから、瀘過筒(8)の下段空間に出るものである。
【0010】
図2は、瀘布(4)の構造を示す説明図である。即ち、瀘布の側面下部および底面部に、適当な分布で切り込み(切れ目)(A)を入れた構造である。この切り込みの大きさは、回収すべきスラッジの長径より小さい幅で、該長径より大きい長さのものである。即ち、固液分離が効率的に且つ迅速に行われるように、瀘別すべきスラッジの大きさ、特性を考慮して、以上のような切り込みを入れた瀘布を用いるものである。当初は、発明者は、ほぼ円形の孔を設けて試したが、効率的な分離は得られなかった。
【0011】
そして、切り込みの分布状態は、処理液が十分な瀘過速度になるものにする。即ち、これは、処理すべき液を、試しに瀘過させて、分布状態を決めることができるものである。
【0012】
本発明によると、処理液を、以上のような切り込み(A)を多数有する瀘布(4)を十分な速度で通過、循環させる。その処理液の循環を、スラッジが、処理液になくなるまで、行う。スラッジが、瀘布(4)の内部にたまるにつれて、流量が落ちていくが、例えば、初期には、100〜120l/分の流量が、20〜15l/分に落ちたところで、ロ過作業すなわち、循環を止める。
【0013】
図3は、本発明により、固液分離のための瀘過が行われる様子を、示す断面図である。即ち、本発明による瀘布(4)は、3層のネット(網)(7)とともに設けられている。そして、処理液Bは、矢印のように、本発明の瀘布(4)を通過して、3層のネット(7)の中を矢印のように流れ、瀘過バスケット(6)の下部穴(6−1)から、流れ出る。従って、処理液は、瀘布(4)の底面或いは低部だけでなく、上部側面からも流れ出る。処理液は、瀘布(4)の底面及び低部側面の切り込みを備えた領域から最も流れ出るが、スラッジは、その部分に最もよく溜り、蓄積していくために、徐々に流量は減少していく。
【0014】
ネット(網)(7)は、上記のように3層のネット、網であり、ポリエチレンなどの樹脂で形成されたものである。例示のものは、3層であるが、必要に応じて、2層でも4層でもよい。
【0015】
図4は、瀘布(4)の上に蓄積なれたスラッジ(13)とその乾燥方法を示す説明断面図である。処理液を循環させて、ある程度、固液分離した形で、スラッジが、図示のように、瀘布(4)の上に蓄積されると、液入口(1)のバルブ、液出口(10)のバルブを閉める。そして、上部空間に設けた空気孔(11)のバルブ及び 瀘過筒(8)の側面に設けた吸引口(12)のバルブを開ける。次に、吸引口のバルブより真空ポンプに接続し、真空吸引する。すると、瀘過筒(8)の中の下段空間から真空吸引されて、瀘過バスケット(6)の中は真空に近い状態となり、スラッジ(13)内部の水分が瀘布外に矢印で示すように瀘布(4)から出る。そして、3層のネット(網)(7)を通り、バスケット(6)の底面の孔から出て、瀘過筒(8)の下段に水分が溜まる。
【0016】
図4に示すように、真空吸引すると、蓄積されたスラッジ(13)内の水分も同時に吸引され、スラッジは乾燥される。次に、スラッジの堆積され乾燥された瀘布に対して、次に、上蓋(2)を取り除き、そして、瀘布押さえ(3)を取り除き、瀘布(4)を裏返して、瀘布についたスラッジ(13)をふるい落として、有用で価値のある金属スラッジを、簡単に且つ迅速、容易に、回収することができる。
【0017】
本発明による瀘布の製造には、ポリオレフィン系合成繊維、例えば、パイレン(登録商標)などで織った日本合織工業製の品番P−2304などを用いることができる。
【0018】
また、本発明の脱水瀘過装置に、瀘布(4)とともに用いられる3層のネット(網)(7)の材質は、ポリエチレン樹脂のネットである。
【0019】
【発明の効果】
本発明のスラッジ回収瀘布およびそれによるロ過装置は、以上のような構成により、次のごとき技術的効果があった。
第1に、電解スラッジのような有用で価値があるが、瀘布の目を詰まらせ、効率的に瀘過処理できない沈殿物でも、容易に且つ効率よく、瀘別分離できる。
第2に、従って、目詰まりがなく、ある程度の速度で電解処理液を瀘別分離することができる装置を提供した。
【図面の簡単な説明】
【図1】本発明による脱水瀘過装置の断面図である。
【図2】本発明による瀘布の構造を示す斜視図である。
【図3】本発明の瀘布を通す瀘過の様子を示す模式断面図である。
【図4】本発明の瀘布により蓄積されたスラッジとその真空吸引の様子を示す模式的断面図である。
【符号の説明】
1 処理液入口 2 上蓋
3 瀘布押え 4 瀘布
5 中間輪 6 バスケット
7 ネット 8 瀘筒
9 底蓋 10 液出口
11 空気取入口 12 吸引口
13 瀘布上にたまったスラッジ
A 瀘布に開けた穴 B 処理液
C 瀘布通過液 D 空気
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a sludge recovery filter applied to various suspensions frequently generated by industrial activities and the like, in particular, a filtration treatment from a plating solution, and a dewatering filter using the sludge recovery filter. About. That is, the present invention provides a sludge collection filter cloth for filtering a plating bath solution (including a plating stripping solution and a plating stripping solution) used to some extent and collecting valuable sludge contained therein, and the sludge collection. The present invention relates to a dehydration filter using a filter cloth.
[0002]
[Prior art]
There are various conventional filtration techniques such as gravity filtration, pressure filtration, and suction filtration. In recent years, many techniques using various membranes, filters, and filter cloths have been studied. However, when used to clean the suspended filtrate due to the peeling of the plating film and at the same time to collect valuable metal sludge, it clogged and found no good filter cloth and filtration equipment. .
[0003]
At present, the sludge collecting filter cloth is apt to be clogged in the conventional gravity filtration apparatus because the filter medium and the filter tank are integrated, and it is troublesome to solve the problem. Although there was a lot of work required, an immersion type gravity filtration device for performing filtration by liquid pressure difference has been proposed (see Japanese Patent Application Laid-Open No. 2000-189718). However, with the conventional filter cloth, solid and liquid cannot be separated efficiently and at high speed even with sludge and sediment which are likely to cause clogging.
[0004]
[Problems to be solved by the invention]
An object of the present invention is to provide a sludge collecting filter and a dewatering filter using the same. That is, the present invention is to efficiently and quickly treat and collect useful and valuable sludge. At the same time, the present invention is for economically and rapidly recovering useful metals from a plating solution containing useful plating metal sludge.
[0005]
[Means for Solving the Problems]
The present inventor has made intensive studies to solve the above-mentioned problems. As a result, it has been solved by the following means.
(1) Sludge provided with cuts having a width smaller than the major axis of the sludge to be recovered and a length greater than the major axis only in the bottom portion and the lower portion of the side surface of the filter cloth in a distribution such that a sufficient filtration rate is obtained. A filter cloth for solid-liquid separation, which is used in a dehydration filter to circulate and treat a treatment liquid containing the sludge for filtration and recovery, and to separate the liquid and solid. .
[0006]
(2) Filter cloth for solid-liquid separation in which the width of the cut is smaller than the largest major axis of the sludge to be recovered, and the length of the cut is larger than the largest major axis.
(3) Filters provided with cuts having a width smaller than the major axis of the sludge to be recovered and a length greater than the major axis are formed only in the lower portion of the bottom and side surfaces of the filter cloth in such a distribution that a sufficient filtration rate is obtained. A dewatering filtration device for solid-liquid separation, comprising a cloth, wherein the treatment liquid containing the sludge is circulated for treatment to be used for solid-liquid separation.
[0007]
Hereinafter, an example of the sludge collecting filter cloth of the present invention and a dewatering filter apparatus using the same will be described, but the present invention is not limited thereby.
According to the present invention, the cut (A) having a width smaller than the major axis of the sludge to be recovered and having a length greater than the major axis is formed only in the lower portion of the bottom and side faces of the filter cloth in a distribution state in which a sufficient filtration rate is obtained. With this arrangement, the sludge filtration and collection can be efficiently performed. That is, the cut (A) has a slender shape in which sludge to be filtered is long, and at a long diameter thereof, the filter cloth is clogged with eyes and a large amount of sludge is randomly arranged. When deposited on the filter cloth, the deposited sludge itself is clogged, and the liquid cannot be processed smoothly. Therefore, according to the present invention, a large number of the prescribed holes are provided in the filter cloth, and even if there is sludge passing therethrough, most of the sludge to be recovered is not clogged, and most of the sludge to be recovered is deposited by circulation several times. It is trapped in sludge, deposited and collected. That is, the present invention relates to a filter cloth for collecting and dewatering useful sludge while partially circulating the processing liquid, and a dewatering filtration apparatus using the same.
[0008]
ADVANTAGE OF THE INVENTION According to this invention, while using a normal filter cloth, there is no clogging, a filtration speed can be ensured, and a filtration circulation speed is increased, and most sludge can be efficiently and rapidly collected. . That is, the width of the cut is smaller than the largest major axis of the sludge to be collected, and the length of the cut is larger than the largest major axis, so that the processing liquid can be quickly clogged without clogging the filter cloth. The solid-liquid can be quickly separated by circulating.
[0009]
BEST MODE FOR CARRYING OUT THE INVENTION
FIG. 1 is a schematic cross-sectional view of a dewatering filtration apparatus for sludge recovery according to the present invention.
The treatment liquid B enters the upper space of the filter cylinder (8) from the inlet (1), passes through the filter presser plate (3) having the passage hole (3-1), and enters the filter cloth (4). enter. Then, the liquid that has passed through the filter cloth (4) passes through a net (7), enters the lower space of the filter tube (8) through a hole at the lower part of the filter basket (6), and then passes through a liquid outlet ( From 10), go outside. The net (7) has a three-layer structure (see FIG. 4), and the liquid that has passed through the side of the filter cloth (4) passes between the three-layer network (7) and is filtered. It reaches the lower hole (6-1) of the filtration basket (6), from which it goes out to the lower space of the filtration tube (8).
[0010]
FIG. 2 is an explanatory view showing the structure of the filter cloth (4). That is, the filter cloth has a structure in which cuts (cuts) (A) are formed in the lower side and the bottom of the filter cloth with an appropriate distribution. The size of the cut has a width smaller than the major axis of the sludge to be collected and a length larger than the major axis. That is, the filter cloth cut as described above is used in consideration of the size and characteristics of the sludge to be filtered so that the solid-liquid separation is performed efficiently and quickly. Initially, the inventor tried with a substantially circular hole, but did not achieve efficient separation.
[0011]
Then, the distribution of the cuts is such that the processing liquid has a sufficient filtration rate. That is, it is possible to determine the distribution state by filtering the liquid to be treated on a trial basis.
[0012]
According to the present invention, the treatment liquid is passed and circulated at a sufficient speed through the filter cloth (4) having a large number of cuts (A) as described above. The circulation of the processing liquid is performed until sludge is not present in the processing liquid. As the sludge accumulates inside the filter cloth (4), the flow rate decreases. For example, initially, when the flow rate of 100 to 120 l / min drops to 20 to 15 l / min, the filtration operation is performed. Stop the circulation.
[0013]
FIG. 3 is a cross-sectional view showing how filtration for solid-liquid separation is performed according to the present invention. That is, the filter cloth (4) according to the present invention is provided with a three-layer net (net) (7). Then, the processing liquid B passes through the filter cloth (4) of the present invention as shown by the arrow, flows through the three-layer net (7) as shown by the arrow, and passes through the lower hole of the filtration basket (6). It flows out from (6-1). Therefore, the processing liquid flows out not only from the bottom or lower part of the filter cloth (4) but also from the upper side. The treatment liquid flows most out of the area provided with cuts in the bottom and lower side of the filter cloth (4), but the sludge gradually accumulates and accumulates in that area, so that the flow rate gradually decreases. Go.
[0014]
The net (net) (7) is a three-layer net or net as described above, and is formed of a resin such as polyethylene. The illustrated one has three layers, but may have two or four layers as needed.
[0015]
FIG. 4 is an explanatory sectional view showing the sludge (13) accumulated on the filter cloth (4) and the drying method thereof. When sludge is accumulated on the filter cloth (4) as shown in the figure by circulating the treatment liquid to a certain extent and solid-liquid separated, a valve at the liquid inlet (1) and a liquid outlet (10) are formed. Close the valve. Then, the valve of the air hole (11) provided in the upper space and the valve of the suction port (12) provided on the side surface of the filtration tube (8) are opened. Next, it is connected to a vacuum pump through a valve at the suction port, and vacuum suction is performed. Then, a vacuum is sucked from the lower space in the filtration tube (8), and the inside of the filtration basket (6) is close to a vacuum, and the water inside the sludge (13) is outside the filter cloth as shown by an arrow. Then, the filter cloth (4) comes out. Then, the water passes through the three-layer net (net) (7), exits through the hole in the bottom of the basket (6), and accumulates in the lower stage of the filtration tube (8).
[0016]
As shown in FIG. 4, when vacuum suction is performed, the accumulated water in the sludge (13) is also sucked at the same time, and the sludge is dried. Next, for the filter cloth on which sludge had been deposited and dried, the top cover (2) was then removed, and the filter presser (3) was removed, and the filter cloth (4) was turned over and the filter cloth was attached. By sifting the sludge (13), useful and valuable metal sludge can be collected easily, quickly and easily.
[0017]
In the production of the filter cloth according to the present invention, a polyolefin-based synthetic fiber, for example, a product number P-2304 manufactured by Nippon Kaso Kogyo woven with Pyrene (registered trademark) or the like can be used.
[0018]
The material of the three-layer net (net) (7) used with the filter cloth (4) in the dewatering filtration apparatus of the present invention is a polyethylene resin net.
[0019]
【The invention's effect】
The sludge collecting filter cloth of the present invention and the filter apparatus using the same have the following technical effects by the above-described configuration.
First, precipitates that are useful and valuable, such as electrolytic sludge, but which clog filter cloth and cannot be filtered efficiently can be easily and efficiently filtered off.
Secondly, the present invention provides an apparatus capable of filtering and separating an electrolytic solution at a certain speed without clogging.
[Brief description of the drawings]
FIG. 1 is a sectional view of a dehydration filtration apparatus according to the present invention.
FIG. 2 is a perspective view showing a structure of a filter cloth according to the present invention.
FIG. 3 is a schematic sectional view showing a state of filtration through a filter cloth of the present invention.
FIG. 4 is a schematic cross-sectional view showing sludge accumulated by the filter cloth of the present invention and a state of vacuum suction.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Processing liquid inlet 2 Top lid 3 Filter cloth holder 4 Filter cloth 5 Intermediate wheel 6 Basket 7 Net 8 Filter tube 9 Bottom lid 10 Liquid outlet 11 Air intake 12 Suction port 13 Sludge A accumulated on filter cloth Opened to filter cloth Hole B Treatment liquid C Filtration liquid D Air

Claims (3)

瀘布の底面及び側面の低部のみに、回収すべきスラッジの長径より小さい幅で、該長径より大きい長さの切り目を、十分な瀘過速度になる分布状態で設けた、スラッジ瀘別回収のために、該スラッジを含有する処理液を循環して処理して、固液分離するために、脱水瀘過装置において、使用することを特徴とする固液分離のための瀘布。Sludge filtration and recovery in which only cuts having a width smaller than the major axis of the sludge to be collected and a length larger than the major axis are provided only in the lower part of the bottom and side surfaces of the filter cloth in a distribution state that provides a sufficient filtration speed. A filter cloth for solid-liquid separation, wherein the filter cloth is used in a dehydration filtration apparatus for circulating the processing liquid containing the sludge for solid-liquid separation. 切り目の幅は、回収すべきスラッジの最も大きい長径より小さく、そして、切り目の長さは、該最大長径より大きいことを特徴とする請求項1記載の固液分離のための瀘布。The filter cloth for solid-liquid separation according to claim 1, wherein the width of the cut is smaller than the largest major axis of the sludge to be recovered, and the length of the cut is larger than the maximum major axis. 瀘布の底面及び側面の低部のみに、回収すべきスラッジの長径より小さい幅で、該長径より大きい長さの切り目を、十分な瀘過速度になる分布状態で設けた、瀘布を備えて、該スラッジを含有する処理液を循環して処理して、固液分離するために使用することを特徴とする固液分離のための脱水瀘過装置。Only the lower part of the bottom and side faces of the filter cloth is provided with filter cloth having cuts having a width smaller than the major axis of the sludge to be recovered and having a length larger than the major axis in such a distribution that a sufficient filtration speed is obtained. A dewatering filtration device for solid-liquid separation, wherein the treatment liquid containing the sludge is circulated and processed to be used for solid-liquid separation.
JP2002346199A 2002-11-28 2002-11-28 Sludge collection cloth and dewatering filter using the same Expired - Lifetime JP3796737B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006116540A (en) * 2004-10-25 2006-05-11 W Morgan Howard Fluid filter having filter basket and filtering method
CN106045268A (en) * 2016-08-05 2016-10-26 北京良乡蓝鑫水利工程设计有限公司 Sludge dehydration device
JP2021065830A (en) * 2019-10-21 2021-04-30 Icn株式会社 Filtration device
CN114105423A (en) * 2021-09-27 2022-03-01 韶关鹏瑞环保科技有限公司 High-efficiency impurity-removing pulping method for recoverable sludge

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Publication number Priority date Publication date Assignee Title
CN109499831A (en) * 2018-11-22 2019-03-22 南京蔚岚环境技术研究院有限公司 Filter is used in a kind of anticlogging non-rice habitats mechanic catalyzer processing

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006116540A (en) * 2004-10-25 2006-05-11 W Morgan Howard Fluid filter having filter basket and filtering method
CN106045268A (en) * 2016-08-05 2016-10-26 北京良乡蓝鑫水利工程设计有限公司 Sludge dehydration device
JP2021065830A (en) * 2019-10-21 2021-04-30 Icn株式会社 Filtration device
JP7420340B2 (en) 2019-10-21 2024-01-23 Icn株式会社 filtration device
CN114105423A (en) * 2021-09-27 2022-03-01 韶关鹏瑞环保科技有限公司 High-efficiency impurity-removing pulping method for recoverable sludge

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